Address: 1100 Frederick Lane
City: Morgantown
State: WV
Postal Code: 26508

CO2 equivalent emissions from facility subparts C-II, SS, and TT (metric tons):167,542.7
CO2 equivalent emissions from supplier subparts LL-QQ (metric tons):
Biogenic CO2 emissions from facility subparts C-II, SS, and TT (metric tons):0
Cogeneration Unit Emissions Indicator:N
GHG Report Start Date:2020-01-01
GHG Report End Date:2020-12-31
Description of Changes to Calculation Methodology:
Plant Code Indicator:N
Primary NAICS Code:486210
Second Primary NAICS Code:

Parent Company Details:

Subpart W: Petroleum and Natural Gas Systems

SubpartWSummaryDetails:

Industry Segment Number	9
Industry Segment Name	Onshore petroleum and natural gas gathering and boosting [98.230(a)(9)]
Total Reported CO2 Emissions (mt CO2)	106663.7
Total CO2e Emissions (mt CO2e)	167542.7
Total Reported CH4 Emissions (mt CH4)	2432.67
Total Reported N2O Emissions (mt N2O)	0.209

SubpartWSourceReportingFormRowDetails:

Source Reporting Form	Onshore Production [98.236(aa)(1)]
Required for Selected Industry Segment	No
Source Reporting Form	Facility Overview [98.236(aa)(2-11)]
Required for Selected Industry Segment	Yes
Source Reporting Form	Natural Gas Pneumatic Devices [98.236(b)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	4.1
Total Reported CH4 Emissions (mt CH4)	566.33
Source Reporting Form	Natural Gas Driven Pneumatic Pumps [98.236(c)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.8
Total Reported CH4 Emissions (mt CH4)	103.80
Source Reporting Form	Acid Gas Removal Units [98.236(d)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.0
Source Reporting Form	Dehydrators [98.236(e)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	2230.8
Total Reported CH4 Emissions (mt CH4)	1576.53
Total Reported N2O Emissions (mt N2O)	0.013
Source Reporting Form	Well Venting for Liquids Unloading [98.236(f)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Source Reporting Form	Completions and Workovers with Hydraulic Fracturing [98.236(g)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Completions and Workovers without Hydraulic Fracturing [98.236(h)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Blowdown Vent Stacks [98.236(i)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	1.3
Total Reported CH4 Emissions (mt CH4)	163.62
Source Reporting Form	Atmospheric Storage Tanks [98.236(j)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Transmission Storage Tanks [98.236(k)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Well Testing [98.236(l)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Associated Gas Venting and Flaring [98.236(m)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Flare Stacks [98.236(n)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Centrifugal Compressors [98.236(o)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Source Reporting Form	Reciprocating Compressors [98.236(p)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.7
Total Reported CH4 Emissions (mt CH4)	4.37
Source Reporting Form	Equipment Leaks Surveys and Population Counts [98.236(q,r)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	0.1
Total Reported CH4 Emissions (mt CH4)	16.05
Source Reporting Form	Offshore Petroleum and Natural Gas Production [98.236(s)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Total Reported CH4 Emissions (mt CH4)	0.00
Total Reported N2O Emissions (mt N2O)	0.000
Source Reporting Form	Enhanced Oil Recovery Injection Pumps [98.236(w)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Source Reporting Form	Enhanced Oil Recovery Hydrocarbon Liquids [98.236(x)]
Required for Selected Industry Segment	No
Total Reported CO2 Emissions (mt CO2)	0.0
Source Reporting Form	Combustion Equipment at Onshore Petroleum and Natural Gas Production Facilities, Onshore Petroleum and Natural Gas Gathering and Boosting Facilities, and Natural gas Distribution Facilities [98.236(z)]
Required for Selected Industry Segment	Yes
Total Reported CO2 Emissions (mt CO2)	104425.9
Total Reported CH4 Emissions (mt CH4)	1.97
Total Reported N2O Emissions (mt N2O)	0.197

FacilityOverviewDetails:


FacilityOverviewOnshorePetroleumAndNaturalGasGatheringAndBoostingRowDetails:

Select the basin associated with this facility [98.236(a)(9)]	160A - Appalachian Basin (Eastern Overthrust Area)
Quantity of gas received by the gathering and boosting facility in the calendar year (thousand standard cubic feet) [98.236(aa)(10)(i)]	506436338
Quantity of gas transported to a natural gas processing facility, a natural gas transmission pipeline, a natural gas distribution pipeline, or another gathering and boosting facility in the calendar year (thousand standard cubic feet) [98.236(aa)(10)(ii)]	504246025
Quantity of all hydrocarbon liquids received by the gathering and boosting facility in the calendar year (barrels) [98.236(aa)(10)(iii)]	0
Quantity of all hydrocarbon liquids transported to a natural gas processing facility, a natural gas transmission pipeline, a natural gas distribution pipeline, or another gathering and boosting facility in the calendar year (barrels) [98.236(aa)(10)(iv)]	0

PneumaticDeviceVentingDetails:

mt CO2	4.1
mt CH4	566.33
Did the Facility have any continuous high-bleed pneumatic devices subject to reporting under 98.232 [98.236(b)]?	No
Did the Facility have any intermittent bleed pneumatic devices subject to reporting under 98.232 [98.236(b)]?	Yes
Did the Facility have any continuous low-bleed pneumatic devices subject to reporting under 98.232 [98.236(b)]?	No
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No

PneumaticDeviceTypesRowDetails:

Type of Pneumatic Device	High-bleed Pneumatic Devices
Type of Pneumatic Device	Intermittent Bleed Pneumatic Devices
Total Number, Countt [98.236(b)(1)(i)]	258
Is the Total Number estimated? (Yes / No) [98.236(b)(1)(ii)]	No
Total CO2 Emissions (mt CO2) [98.236(b)(3)]	4.136743
Total CH4 Emissions (mt CH4) [98.236(b)(4)]	566.3258171
Estimated average number of hours in the calendar year that the pneumatic devices were operating, Tt (hours) [98.236(b)(2)]	8784
Type of Pneumatic Device	Low-Bleed Pneumatic Devices

NaturalGasDrivenPneumaticPumpsDetails:

mt CO2	0.8
mt CH4	103.80
Did the Facility have any natural gas driven pneumatic pumps subject to reporting under 98.232 [98.236(c)]?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No

PneumaticPumpTypesRowDetails:

Type of Pneumatic Pump	Natural Gas Driven Pneumatic Pumps
Total count of natural gas driven pneumatic pumps, Count [98.236(c)(1)]	48
Average estimated number of hours in the calendar year that the natural gas driven pneumatic pumps were operated, T (hours) [98.236(c)(2)]	8784
Total CO2 Emissions (mt CO2) [98.236(c)(3)]	0.7582247
Total CH4 Emissions (mt CH4) [98.236(c)(4)]	103.8020102

AcidGasRemovalUnitsDetails:

mt CO2	0.0
Did the Facility have any acid gas removal units that vent directly to the atmosphere, to a flare or engine, or to a sulfur recovery plant subject to reporting under 98.232 [98.236(d)]?	No

DehydratorsDetails:

mt CO2	2230.8
mt CH4	1576.53
mt N2O	0.013
Did the facility have any glycol dehydrators with annual average daily natural gas throughputs greater than or equal to 0.4MMscfd subject to reporting under 98.232 [98.236(e)]?	Yes
Did the facility have any glycol dehydrators with annual average daily natural gas throughputs less than 0.4MMscfd subject to reporting under 98.232 [98.236(e)]?	No
Did the facility have any desiccant dehydrators subject to reporting under 98.232 [98.236(e)]?	No
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No

SmallGlycolDehydrators:

Emissions vented to flare or regenerator firebox/fire tubes

Emissions that were not vented to a flare or regenerator firebox/fire tubes

DessicantDehydrators:

Emissions vented to flare or regenerator firebox/fire tubes

Emissions that were not vented to a flare or regenerator firebox/fire tubes

GlycolDehydratorsMoreThanSpecifiedValueRowDetails:

Unit ID or Name [98.236(e)(1)(i)]	Beaty Dehy 1
County and State [98.236(e)(1)(xviii)]	MARION, WV
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	4.0320238
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	27.8434248
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	0.7
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	71.17
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	795.83
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.0018001
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9539318
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	57.8176269
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	18.7091932
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0002579
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	0.0383153
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.3393886
Unit ID or Name [98.236(e)(1)(i)]	Coopers Run Dehy 1
County and State [98.236(e)(1)(xviii)]	MONONGALIA, WV
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	33.503349
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	29.4959207
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.55
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	6600
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	78.89
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1031.67
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.002267
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9670278
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	199.830988
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	67.483254
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0009072
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	0.199498
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.9887297
Unit ID or Name [98.236(e)(1)(i)]	Coopers Run Dehy 2
County and State [98.236(e)(1)(xviii)]	MONONGALIA, WV
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	42.105431
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	30.5598564
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.74
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	6600
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1031.67
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.002267
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9670278
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	214.5584928
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	72.4580525
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0009741
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	0.2245163
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	1.0777111
Unit ID or Name [98.236(e)(1)(i)]	Daybrook Dehy 1
County and State [98.236(e)(1)(xviii)]	MARION, WV
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	29.2146626
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	36.8755601
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	2.63
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	82.83
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	900.58
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.0038336
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9727315
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	237.4539237
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	80.5509605
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0020556
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	No
Unit ID or Name [98.236(e)(1)(i)]	Hamilton Dehy 1
County and State [98.236(e)(1)(xviii)]	MONONGALIA, WV
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	45.9623818
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	35.6531658
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.44
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	Yes
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8301.1
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	82.58
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	931.25
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.0026001
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9668989
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	303.6384551
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	101.9625777
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0013723
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	1.4205618
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	139.9126278
Unit ID or Name [98.236(e)(1)(i)]	Hamilton Dehy 2
County and State [98.236(e)(1)(xviii)]	MONONGALIA, WV
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	46.0521287
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	35.6531658
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	3.46
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	Yes
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	82.58
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	931.25
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.0026001
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9668989
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	323.1597441
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	108.5181796
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0014606
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	1.5054878
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	148.0622338
Unit ID or Name [98.236(e)(1)(i)]	Wetzel Dehy 1
County and State [98.236(e)(1)(xviii)]	WETZEL, WV
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	2.4432467
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	28.1377049
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	0.7
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	No
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	70
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	745.83
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.0022762
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9482138
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	54.7460672
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	17.3915206
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0002422
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	0.0443493
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	0.3333064
Unit ID or Name [98.236(e)(1)(i)]	Mepco Dehy 1
County and State [98.236(e)(1)(xviii)]	MONONGALIA, WV
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	81.9035943
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	30.9673212
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	6.12
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	Yes
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	1012.5
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.0027127
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9688935
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	439.6591701
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	274.4325496
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.002836
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	1.8227663
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	149.6712927
Unit ID or Name [98.236(e)(1)(i)]	Mepco Dehy 2
County and State [98.236(e)(1)(xviii)]	MONONGALIA, WV
Glycol dehydrator feed natural gas flow rate determined by engineering estimate based on best available data (MMscfd) [98.236(e)(1)(ii)]	80.1508735
Dehydrator feed natural gas water content (pounds per MMscf) [98.236(e)(1)(iii)]	31.2842382
Dehydrator outlet natural gas water content (pounds per MMscf) [98.236(e)(1)(iv)]	7
Glycol dehydrator absorbent circulation pump type [98.236(e)(1)(v)]	Natural gas pneumatic
Dehydrator absorbent circulation rate (gallons per minute) [98.236(e)(1)(vi)]	5.55
Report type of absorbent used [98.236(e)(1)(vii)]	Triethylene glycol (TEG)
Report whether stripper gas is used in glycol dehydrator [98.236(e)(1)(viii)]	Yes
Report whether a flash tank separator is used in glycol dehydrator [98.236(e)(1)(ix)]	Yes
Total time the glycol dehydrator is operating (hours) [98.236(e)(1)(x)]	8784
Temperature of the wet natural gas (°F) [98.236(e)(1)(xi)]	80
Pressure of the wet natural gas (psig) [98.236(e)(1)(xii)]	997.92
Concentration of CO2 in wet natural gas (mole fraction) [98.236(e)(1)(xiv)]	0.0027127
Concentration of CH4 in wet natural gas (mole fraction) [98.236(e)(1)(xiii)]	0.9688935
Were any dehydrator emissions vented to a vapor recovery device? [98.236(e)(1)(xv)]	No
Were any dehydrator emissions vented to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvi)]	Yes
CO2 Emissions from Flares or Regenerators (mt CO2) [98.236(e)(1)(xvi)(A)]	392.8711636
CH4 Emissions from Flares or Regenerators (mt CH4) [98.236(e)(1)(xvi)(B)]	245.2175298
N2O Emissions from Flares or Regenerators (mt N2O) [98.236(e)(1)(xvi)(C)]	0.0025329
Were any dehydrator emissions vented to the atmosphere without being routed to a flare or regenerator firebox/fire tubes? [98.236(e)(1)(xvii)]	Yes
CO2 Emissions from Venting (mt CO2) [98.236(e)(1)(xvii)(A)]	1.8080175
CH4 Emissions from Venting (mt CH4) [98.236(e)(1)(xvii)(B)]	149.4162103

BlowdownVentStacksDetails:

mt CO2	1.3
mt CH4	163.62
Did the facility have any blowdown vent stacks subject to reporting under 98.232 [98.236(i)]?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No
How were emissions determined? [98.236(i)]	Calculated by equipment or event type

BlowdownEquipmentOrEventEmissionsRowDetails:

Equipment or event type [98.236(i)(1)] [98.236(i)(2)]	Facility piping
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	0
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	0
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]	Pipeline venting
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	0
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	0
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]	Compressors
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	302
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.9424885
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	121.1460037
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]	Scrubbers/strainers
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	1
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.0000143
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	0.0022277
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]	Pig launchers and receivers
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	81
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.0094743
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	1.4751635
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]	Emergency shutdowns
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	4
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0.3139365
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	40.9978824
Equipment or event type [98.236(i)(1)] [98.236(i)(2)]	All other equipment with a physical volume greater than or equal 50 cubic feet
Total number of blowdowns for equipment or event type, N [98.236(i)(1)(i)]	0
Annual total CO2 emissions for each equipment or event type (mt CO2) [98.236(i)(1)(ii)]	0
Annual total CH4 emissions for each equipment or event type (mt CH4) [98.236(i)(1)(iii)]	0

AtmosphericTanksDetails:

mt CO2	0.0
mt CH4	0.00
mt N2O	0.000
Did the facility send hydrocarbon liquids to atmospheric storage tanks that are subject to reporting under 98.232 [98.236(j)]?	No

FlareStacksDetails:

mt CO2	0.0
mt CH4	0.00
mt N2O	0.000
Did the facility have flare stacks subject to reporting under 98.232 [98.236(n)]?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No

UniqueFlareStacksRowDetails:

Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	Beaty Reboiler
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	2087868.96
Flare combustion efficiency (decimal value) [98.236(n)(6)]	1
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.9334275
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0042059
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0.5
CO2 emissions (mt CO2) [98.236(n)(9)]	0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	Coopers #1 Reboiler
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	7345998
Flare combustion efficiency (decimal value) [98.236(n)(6)]	1
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.9569164
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0049305
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0.5
CO2 emissions (mt CO2) [98.236(n)(9)]	0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	Coopers #2 Reboiler
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	7887198
Flare combustion efficiency (decimal value) [98.236(n)(6)]	1
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.9569576
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0049279
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0.5
CO2 emissions (mt CO2) [98.236(n)(9)]	0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	Daybrook Reboiler - Flash
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	8649165.6
Flare combustion efficiency (decimal value) [98.236(n)(6)]	1
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.9618742
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0083513
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0.5
CO2 emissions (mt CO2) [98.236(n)(9)]	0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	Daybrook Reboiler - Regen
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	7995372.48
Flare combustion efficiency (decimal value) [98.236(n)(6)]	1
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.0089197
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0011488
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0.5
CO2 emissions (mt CO2) [98.236(n)(9)]	0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	Hamilton #1 Reboiler
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	11112133.65
Flare combustion efficiency (decimal value) [98.236(n)(6)]	1
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.9558112
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0056539
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0.5
CO2 emissions (mt CO2) [98.236(n)(9)]	0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	Hamilton #2 Reboiler
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	11826514.08
Flare combustion efficiency (decimal value) [98.236(n)(6)]	1
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.9558165
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0056531
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0.5
CO2 emissions (mt CO2) [98.236(n)(9)]	0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	Wetzel Reboiler
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	1960940.16
Flare combustion efficiency (decimal value) [98.236(n)(6)]	1
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.9238511
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.005368
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0.5
CO2 emissions (mt CO2) [98.236(n)(9)]	0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	Mepco #1 Reboiler
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	22963835.52
Flare combustion efficiency (decimal value) [98.236(n)(6)]	1
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.9575834
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0059338
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0.65
CO2 emissions (mt CO2) [98.236(n)(9)]	0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0
Unique Name or ID Number for the Flare Stack [98.236(n)(1)]	Mepco #2 Reboiler
Does the flare stack have a continuous flow monitor on gas to the flare? [98.236(n)(2)]	No
Does the flare stack have a continuous gas analyzer on gas to the flare? [98.236(n)(3)]	No
Were CEMS used to measure CO2 emissions for the flare stack? [98.233(n)(8)] [98.236(n)(12)]	No
Volume of gas sent to flare, Vs (standard cubic feet) [98.236(n)(4)]	20509322.4
Flare combustion efficiency (decimal value) [98.236(n)(6)]	1
Mole fraction of CH4 in flare feed gas, XCH4 [98.236(n)(7)]	0.9580444
Mole fraction of CO2 in flare feed gas, XCO2 [98.236(n)(8)]	0.0059277
Fraction of feed gas sent to un-lit flare, Zu [98.236(n)(5)]	0.65
CO2 emissions (mt CO2) [98.236(n)(9)]	0
CH4 Emissions (mt CH4) (Eq. W-19) [98.236(n)(10)]	0
N2O Emissions (mt N2O) (Eq. W-40) [98.236(n)(11)]	0

CentrifugalCompressorsDetails:

mt CO2	0.0
mt CH4	0.00
Did the facility have any centrifugal compressors subject to reporting under 98.232 [98.236(o)]?	No

ReciprocatingCompressorsDetails:

mt CO2	0.7
mt CH4	4.37
Did the facility have any reciprocating compressors subject to reporting under 98.232 [98.236(p)]?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No
Total annual Reciprocating Compressor emissions CO2 Emissions (mt CO2) [98.236(p)(5)(ii)]	0.6652848
Total annual Reciprocating Compressor emissions CH4 Emissions (mt CH4) [98.236(p)(5)(iii)]	4.368384
Count of Reciprocating Compressors [98.236(p)(5)(i)]	24

OtherEmissionsFromEquipmentLeaksDetails:

mt CO2	0.1
mt CH4	16.05
Did this facility use leak surveys to calculate emissions from equipment leaks in accordance with 98.232 [per 98.236(q)]?	Yes
Did this facility use population counts to calculate emissions from equipment leaks in accordance with 98.232 [per 98.236(r)]?	Yes
Did the facility elect to comply with 98.236(q) according to 98.233(q)(1)(iv) for any components at the facility [per 98.236(q)(1)(iv)]?	No
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No
Number of complete equipment leak surveys performed during the calendar year [98.236(q)(1)(i)]	16
Optical gas imaging instrument as specified in §60.18 [98.234(a)(1)]	No
Method 21 [98.234(a)(2)]	No
Infrared laser beam illuminated instrument [98.234(a)(3)]	No
Acoustic leak detection device [98.234(a)(5)]	No
Optical gas imaging instrument as specified in §60.5397a [98.234(a)(6)]	Yes
Method 21 as specified in §60.5397a [98.234(a)(7)]	No
Component count calculation method for all emission source types in Table R.1 other than gathering pipelines [98.236(r)(3)(i)]	Component Count Method 1

OnshorePetroleumAndNaturalGasProductionAndGatheringAndBoostingRowDetails:

Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Gas Service - Valve
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	11
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	2788.3636364
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0203213
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	2.7820103
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Gas Service - Flange
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	1
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	3048
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0016897
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.2313233
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Gas Service - Connector (other)
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	16
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	2917.5
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0082052
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	1.1232974
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Gas Service - Open-Ended Line
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Gas Service - Pressure Relief Valve
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Gas Service - Pump Seal
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	0
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	0
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0
Component Type [98.236(q)(2)(i)]	Onshore Production or GB Components, Gas Service - Other
Total number of surveyed component type identified as leaking, xp [98.236(q)(2)(ii)]	3
Average time the surveyed components are assumed to be leaking and operational, Tp,z (hours) [98.236(q)(2)(iii)]	3112
CO2 Emissions (surveyed components identified as leaking only) (mt CO2) [98.236(q)(2)(iv)]	0.0056805
CH4 Emissions (surveyed components identified as leaking only) (mt CH4) [98.236(q)(2)(v)]	0.7776674

LeaksCalculatedWithCountsFactorsRowDetails:

Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]	Gas Service - Valves
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]	Eastern U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]	114
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8784
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0.0036557
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	0.500474
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]	Gas Service - Connectors
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]	Eastern U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]	453
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8784
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0.0016141
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	0.2209695
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]	Gas Service - Open ended lines
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]	Eastern U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]	4
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8784
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0.0002898
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	0.0396737
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]	Gas Service - Pressure relief valves
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]	Eastern U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]	4
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8784
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0.00019
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	0.0260155
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]	Gathering pipelines - Protected steel gathering pipeline
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]	Eastern U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]	135.48
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	8784
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0.0756272
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	10.3534701
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]	Gathering pipelines - Unprotected steel gathering pipeline
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]	Eastern U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]	0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	0
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]	Gathering pipelines - Plastic/composite gathering pipeline
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]	Eastern U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]	0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	0
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	0
Emission Source Type (Eq. W-32A) [98.232(c)(21)] [98.233(r)]	Gathering pipelines - Cast iron gathering pipeline
Geographic Location (according to Table W-1D) [98.236(r)(1)(i)]	Eastern U.S.
Total number of emission source type, Counte (for gathering pipelines, this value is the number of miles of pipeline per material type) [98.236(r)(1)(ii)]	0
Average estimated time that the emission source type was operational in the calendar year, Te (hours) [98.236(r)(1)(iii)]	0
CO2 Emissions (mt CO2) [98.236(r)(1)(iv)]	0
CH4 Emissions (mt CH4) [98.236(r)(1)(v)]	0

MajorGasEquipmentTypeRowDetails:

Major Equipment Type [98.236(r)(3)(ii)]	Wellhead
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	No
Major Equipment Type [98.236(r)(3)(ii)]	Separators
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	Yes
Count of Major Equipment Type in Eastern US [98.236(r)(3)(ii)(B)]	6
Major Equipment Type [98.236(r)(3)(ii)]	Meters/piping
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	Yes
Count of Major Equipment Type in Eastern US [98.236(r)(3)(ii)(B)]	4
Major Equipment Type [98.236(r)(3)(ii)]	Compressors
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	Yes
Count of Major Equipment Type in Eastern US [98.236(r)(3)(ii)(B)]	1
Major Equipment Type [98.236(r)(3)(ii)]	In-line heaters
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	No
Major Equipment Type [98.236(r)(3)(ii)]	Dehydrators
Equipment type present at facility? [98.236(r)(3)(ii)(A)]	Yes
Count of Major Equipment Type in Eastern US [98.236(r)(3)(ii)(B)]	2

CombustionEmissionsDetails:

mt CO2	104425.9
mt CH4	1.97
mt N2O	0.197
Did the Facility have combustion units subject to reporting under 98.232?	Yes
Were missing data procedures used for any parameters to calculate GHG emissions? [98.235]	No
Are there external fuel combustion units with a rated heat capacity less than or equal to 5 mmBtu/hr? [98.236(z)(1)(i)]	Yes
Are there internal fuel combustion units that are not compressor-drivers, with a rated heat capacity less than or equal to 1 mmBtu/hr? [98.236(z)(1)(i)]	No
Total number of combustion units meeting 98.236(z)(1) descriptions	9
Are there external fuel combustion units with a rated heat capacity greater than 5 mmBtu/hr? [98.236(z)(2)(i)]	No
Are there internal fuel combustion units that are not compressor-drivers, with a rated heat capacity greater than 1 mmBtu/hr? [98.236(z)(2)(i)]	Yes
Are there Internal fuel combustion units of any heat capacity that are compressor-drivers? [98.236(z)(2)(i)]	Yes

LargeCombustionUnitEmissionsRowDetails:

Type of combustion unit [98.236(z)(2)(i)]	Internal fuel combustion units of any heat capacity that are compressor-drivers
Type of fuel combusted [98.236(z)(2)(ii)]	Natural gas
Quantity of fuel combusted in calendar year [98.236(z)(2)(iii)]	1913700
Unit of measure [98.236(z)(2)(iii)	thousand standard cubic feet
CO2 Emissions (mt CO2) [98.236(z)(2)(iv)]	104180.985972
CH4 Emissions (mt CH4) [98.236(z)(2)(v)]	1.9634562
N2O Emissions (mt N2O) [98.236(z)(2)(vi)]	0.1963456
Type of combustion unit [98.236(z)(2)(i)]	Internal fuel combustion units that are not compressor-drivers, with a rated heat capacity greater than 1 mmBtu/hr
Type of fuel combusted [98.236(z)(2)(ii)]	Natural gas
Quantity of fuel combusted in calendar year [98.236(z)(2)(iii)]	4499.704
Unit of measure [98.236(z)(2)(iii)	thousand standard cubic feet
CO2 Emissions (mt CO2) [98.236(z)(2)(iv)]	244.9619059
CH4 Emissions (mt CH4) [98.236(z)(2)(v)]	0.0046167
N2O Emissions (mt N2O) [98.236(z)(2)(vi)]	0.0004617